GB164867A - Improvements in or relating to centrifugal separating apparatus - Google Patents
Improvements in or relating to centrifugal separating apparatusInfo
- Publication number
- GB164867A GB164867A GB809120A GB809120A GB164867A GB 164867 A GB164867 A GB 164867A GB 809120 A GB809120 A GB 809120A GB 809120 A GB809120 A GB 809120A GB 164867 A GB164867 A GB 164867A
- Authority
- GB
- United Kingdom
- Prior art keywords
- chamber
- shaft
- liquid
- openings
- discharge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/10—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
- B04B1/14—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge
- B04B1/16—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge with discharging outlets controlled by the rotational speed of the bowl
- B04B1/18—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with periodical discharge with discharging outlets controlled by the rotational speed of the bowl controlled by the centrifugal force of an auxiliary liquid
Landscapes
- Centrifugal Separators (AREA)
Abstract
164,867. Sturgeon, R. A. March 18, 1920. Density separators; discharging.-In a separating-apparatus relative motion is obtained for discharge purposes, between the chamber and its end wall by the variation of the pressure produced by centrifugal force in a liquid admitted to the space between the movable member and an end cover fixed to the shaft. The chamber B, Fig. 1, has an integral end wall C and can move axially within the fixed dome E, the end C acting as a piston or being connected to the dome by annular diaphragms. The lower end of the chamber engages an annular seating D<1> on the face of the end cover D fixed on the shaft A. Liquid is admitted by the pipe F to the space between the dome E and the chamber end C, and the pressure keeps the chamber upon its seating. The liquid to be treated enters the upper end of the hollow shaft, passes through the openings A<1> over the weir A<2> into the chamber B, and after depositing its solids upon the chamber wall escapes through openings H in the end D and flows into a channel in the foundation of the apparatus. To discharge the solids, the supply of liquid through the pipe F is stopped, and as the liquid passes through the openings E<3> the pressure on the end C diminishes until the springs D<2> raise the chamber B, which is then swilled out to discharge the deposited solids. A filter 0 of any suitable material may be arranged in the chamber as shown. In a modification the chamber is integral with the shaft and the lower end plate is movable and is held in by the pressure of liquid supplied through the pipe F. Two separate sets of openings for the discharge of clarified liquids of different specific gravities are made in the shaft and are separated by a baffle. In another modification a receptacle M, Fig. 3, for grease recovery is placed at the lower end of the shaft; the grease passes through discharge openings M<1> in the shaft into the vessel M and the clarified liquid passes into the annual conduit N. The solids are swilled out as in the arrangement shown in Fig. 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB809120A GB164867A (en) | 1920-03-18 | 1920-03-18 | Improvements in or relating to centrifugal separating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB809120A GB164867A (en) | 1920-03-18 | 1920-03-18 | Improvements in or relating to centrifugal separating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB164867A true GB164867A (en) | 1921-06-20 |
Family
ID=9845573
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB809120A Expired GB164867A (en) | 1920-03-18 | 1920-03-18 | Improvements in or relating to centrifugal separating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB164867A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2749031A (en) * | 1953-06-22 | 1956-06-05 | Beloit Iron Works | Separator-pumping |
| DE3143348A1 (en) * | 1981-10-31 | 1983-05-11 | Deutsche Gesellschaft für Wiederaufarbeitung von Kernbrennstoffen mbH, 3000 Hannover | Centrifuge |
-
1920
- 1920-03-18 GB GB809120A patent/GB164867A/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2749031A (en) * | 1953-06-22 | 1956-06-05 | Beloit Iron Works | Separator-pumping |
| DE3143348A1 (en) * | 1981-10-31 | 1983-05-11 | Deutsche Gesellschaft für Wiederaufarbeitung von Kernbrennstoffen mbH, 3000 Hannover | Centrifuge |
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